CN1273503C - Polypropylene preparation - Google Patents

Polypropylene preparation Download PDF

Info

Publication number
CN1273503C
CN1273503C CN02809985.0A CN02809985A CN1273503C CN 1273503 C CN1273503 C CN 1273503C CN 02809985 A CN02809985 A CN 02809985A CN 1273503 C CN1273503 C CN 1273503C
Authority
CN
China
Prior art keywords
group
activator
catalyzer
polypropylene
inequality
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN02809985.0A
Other languages
Chinese (zh)
Other versions
CN1509296A (en
Inventor
C·C·枚沃顿
S·纳吉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Equistar Chemicals LP
Original Assignee
Equistar Chemicals LP
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Equistar Chemicals LP filed Critical Equistar Chemicals LP
Publication of CN1509296A publication Critical patent/CN1509296A/en
Application granted granted Critical
Publication of CN1273503C publication Critical patent/CN1273503C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
    • C08F297/06—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type
    • C08F297/08—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type polymerising mono-olefins
    • C08F297/083—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type polymerising mono-olefins the monomers being ethylene or propylene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F10/04—Monomers containing three or four carbon atoms
    • C08F10/06—Propene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F297/00—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer
    • C08F297/06—Macromolecular compounds obtained by successively polymerising different monomer systems using a catalyst of the ionic or coordination type without deactivating the intermediate polymer using a catalyst of the coordination type
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F110/04—Monomers containing three or four carbon atoms
    • C08F110/06—Propene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00—Polymerisation catalysts
    • C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62—Refractory metals or compounds thereof
    • C08F4/64—Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/65912—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an organoaluminium compound
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S526/943—Polymerization with metallocene catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

A propylene polymerization process is disclosed. The process gives polypropylene having isotactic and atactic stereoblock sequences. The process is performed in the presence of a non-bridged bisindenoindol-based single-site catalyst. The polypropylene produced has an isotactic pentad (mmmm) content within the range of about 10 mole % to about 70 mole %.

Description

Polyacrylic preparation
Technical field
The present invention relates to polyacrylic preparation.The invention particularly relates to polyacrylic preparation with isotactic block sequence and atactic block sequence.
Background technology
Polypropylene is different from polyethylene, because be connected with a methyl group every a carbon atom on the polypropylene skeleton.According to the position of methyl group, polypropylene can be divided three classes: isotatic polypropylene, syndiotactic polypropylene and Atactic Polypropelene.
Utilize the Zlegler catalyzer make isotatic polypropylene suitability for industrialized production decades.Single-site catalysts also is applicable to the preparation of isotatic polypropylene.For example, WO99/24446 has introduced the single-site catalysts that adopts based on bridging indenoindole base and prepares isotactic content and be higher than 90% polyacrylic method.Isotatic polypropylene forms crystalline structure easily.It has good chemical resistance and thermotolerance, thereby mainly as textile fibres and film.
Different with isotatic polypropylene, Atactic Polypropelene is non-crystalline state.Compare with isotatic polypropylene, Atactic Polypropelene has higher toughness but chemical resistant properties and thermotolerance are relatively poor.It is mainly used in tackiness agent.Though Atactic Polypropelene can directly make (seeing United States Patent (USP) 5945496) by polyreaction, it is the by product in the isotatic polypropylene manufacturing processed normally.
Because isotatic polypropylene and Atactic Polypropelene have complementary character, thereby their mixing are had great importance.But, make the effect of their blend bad with physical method, compatible because they are difficult for.Preparing the polypropylene that has isotactic sequence and random sequence on the same polymer chain simultaneously is a kind of Perfected process that makes these two kinds of mixed with polymers.But, be difficult to find a kind of catalyzer that can alternately form isotactic sequence and random sequence.
United States Patent (USP) 5594080 has been introduced to adopt based on the single-site catalysts preparation of aryl-indenyl not only to have had an isotactic sequence but also had had the polyacrylic method of random sequence.This polypropylene contains the isotactic structure below about 20% or 20%.
United States Patent (USP) 5747621 has also been introduced the polyacrylic preparation that not only comprises the isotactic component but also comprise random component.Yet these components master is if it were not for mixing in the mode on the same polymer chain of being combined in, but with the physics mode blend.
United States Patent (USP) 5756614 has been introduced the polyacrylic method of asymmetric space rigid metal cyclopentadiene Preparation of Catalyst stereoblock that adopts.This catalyzer has two kinds of reactive catalytic centers of tradable different stereochemistry, can make isotactic/atactic block polypropylene thus.This polymkeric substance demonstrates and resembles performance likely the thermoplastic elastic material.Yet this Preparation of Catalyst is very complicated and cost is very high.
In a word, growing to the interest of the polyacrylic method of preparation isotactic-atactic block.The ideal preparation method is that employing obtains easily and the not high single-site catalysts of price.
Summary of the invention
The present invention is a kind of propene polymerizing method.This method adopts the 3-5 group 4 transition metal catalyzer with two non-bridged indenoindole polymerization of olefin using catalyst bodies.This catalyzer is activated.The invention provides the polyacrylic simple but effective method that a kind of preparation has isotaxy and atactic block sequence.Different with known method, the inventive method neither needs complicated bridging catalyzer, does not also need to make isotatic polypropylene and Atactic Polypropelene blend mutually.Isotactic five unit group (mmmm) content in the polypropylene of making are in the about 70 moles of % scopes of about 10 moles of %-, thereby the suitable thermoplastic elastomer (s) of doing.
Embodiment
The inventive method is included under the existence of 3-5 group 4 transition metal catalyzer and makes propylene polymerization.This catalyzer has two indenoindole ylidene ligands.So-called " Indenoindole compounds " is meant a kind of organic compound that has indole ring and indenes ring simultaneously.Two five-rings are mutual condensed, and promptly they share two carbon atoms.Not mutual bridging connects between this indenoindole ylidene ligands.
This catalyzer preferably has following formula:
Figure C0280998500061
M is the 3-5 group 4 transition metal in the formula.Preferred L is a zirconium.Indenoindole ylidene ligands L 1And L 2With π key and M bonding mutually.L 1And L 2Can be identical or inequality and have following selectable structure:
With
Figure C0280998500072
R in the formula 1Be preferably selected from alkyl, aryl, aralkyl and silyl-group.R 1Example be methyl, the tertiary butyl, phenyl and trimethyl silyl group.R 2To R 10Be identical or inequality, and be preferably selected from hydrogen, alkyl, aryl, aralkyl, silyl, halogen, alkoxyl group, aryloxy, siloxy-, thioether, nitro, amino group etc.
This catalyzer has two other X ligand 1And X 2, X 1And X 2Can be identical or inequality.They can be preferably selected from halogen, alkoxyl group, aryloxy, siloxy-, dialkyl amido, ammonia diaryl base and hydrocarbyl group.Variable part such as halogen are particularly preferred.
The catalyzer example that is suitable for comprises two-(2-chloro-5-phenyl-5,10-dihydro indeno [1,2-b] indyl) dichloro closes zirconium (structure I), two-(5-phenyl-5,10-dihydro indeno [1,2-b] indyl) dichloro closes zirconium (structure I I), two-(5,8-dimethyl-5,10-dihydro indeno [1,2-b] indyl) dichloro closes zirconium (structure III) and two-(5-trimethyl silyl-8-methyl-5,10-dihydro indeno [1,2-b] indyl) dichloro closes zirconium (structure I V).
Figure C0280998500081
This catalyzer can prepare by any known method.For example application number is that the common co-pending application of 09/417510 (present US 6232260) has at length introduced how to prepare the catalyst based method of indenoindole, and this content is incorporated herein for reference in full.For example, catalyzer (III) can prepare by following schema:
Figure C0280998500091
This catalyzer is activated.The activator that is suitable for comprises anionic compound and the compound of trialkylboron and triaryl boron and their mixture of aikyiaiurnirsoxan beta, aluminum alkyls, alkyl aluminum halide, boron or aluminium.The example of activator comprises methylaluminoxane (MAO), polymerization aikyiaiurnirsoxan beta (PMAO), ethyl aikyiaiurnirsoxan beta, diisobutyl alumina alkane, triethyl aluminum, diethyl aluminum chloride, trimethyl aluminium, triisobutyl aluminium, four (pentafluorophenyl group) lithium tetraborate, four (pentafluorophenyl group) lithium aluminate, xylidine four (pentafluorophenyl group) borate, trityl four (pentafluorophenyl group) borate, three (pentafluorophenyl group) borine, triphenylborane, three n-octyl borines etc. and their mixture.
The selection of activator is decided by to comprise many factors of isotactic/random ratio in the catalyzer that adopted and the desirable polypropylene product.For example, when adopting two (2-chloro-5-phenyl-5,10-dihydro indeno [1,2-b] indyl) when zirconium dichloride is activator as catalyzer and MAO, polyacrylic isotactic five pentad content of then making are about 50% (seeing embodiment 1), and adopting triisobutyl aluminium and trityl four (pentafluorophenyl group) is boratory when being combined into activator, isotactic five pentad content are about 20% (seeing embodiment 12).
Optional is that catalyzer is fixed on carrier.Preferred carrier is porous material such as inorganic oxide and muriate, and organic polymer resin.Preferred inorganic oxide comprises the oxide compound of the 2nd, 3,4,5,13 or 14 family's elements.Preferred carrier comprises silicon-dioxide, aluminum oxide, silica-alumina, magnesium oxide, titanium dioxide, zirconium white, magnesium chloride and crosslinked polystyrene.
Can adopt various polymerization methodses to implement propylene polymerization.Polymerization process can be in gas phase, in the body, carry out in the solution or in the slurry.Polyreaction can be carried out in very wide temperature range.Preferably, the temperature range of polyreaction is about 0 ℃ to about 150 ℃, more preferably about 25 ℃-Yue 100 ℃.
Utilize the inventive method to make and have the controlled three-dimensional chemical configuration and the polypropylene product of physicals.The invention provides a kind of simple but effective method that can obtain to satisfy isotactic/Atactic Polypropelene ratio requirement.The present invention does not need complicated bridging catalyzer.The polypropylene that the inventive method is made has isotactic five pentad content (the about 70 moles of % of about 10 moles of %-, preferred about 40 moles of %-60 mole %) of wide region, and this polypropylene is suitable as the material of film, tackiness agent and other elastomeric objects.
Following embodiment is just to explanation of the present invention.The person skilled in the art can differentiate the many variants in the present invention's spirit and the claim scope.
Embodiment A
Catalyzer 1: two (2-chloro-5-phenyl-5,10-dihydro indeno [1,2-b] indyl) dichloro closes the preparation of zirconium
In 100 milliliters of round-bottomed flasks, mix 50 milliliters of ethanol, 4 milliliters of H 2SO 4, 5.09 gram 5-chloro-1-indones (0.0306 mole) and 6.74 restrain hydrochloric acid N, N-phenylbenzene hydrazine (0.0306 mole) and reflux 4 hours.When reaction mixture cools off, isolate brown solid, in ethanol, carry out recrystallization and can get 7.55 gram products (yield is 72%).
Under dry nitrogen atmosphere, make 2.37 gram (0.0075 mole) 2-chloro-5-phenyl-5,10-dihydro indeno [1,2-b] indoles forms slurry in 40 milliliters of hexanes.Add the cyclohexane solution of the n-Butyl Lithium of 5.6 milliliters of 2.0 moles/L then to this slurry.Under room temperature and nitrogen atmosphere, stirred this mixture 67 hours.The yellow solid that filtration makes is used hexane wash, dry in a vacuum then (product is 1.8 grams, and yield is 67%).
Above-mentioned lithium salts (0.9 gram, 0.0028 mole) is dissolved in 4 milliliters of toluene and the 0.5 milliliter of diethyl ether mixture.Make zirconium tetrachloride (0.34 gram, 0.0014 mole) in 10 milliliters of diethyl ether and 4 milliliters of toluene mixture, form slurry.Under 25 ℃ and dry nitrogen atmosphere, lithium salt solution is added in this slurry lentamente then, and stirred 40 hours down at 25 ℃.The orange solids that filtration makes, with the diethyl ether washing, dry in a vacuum then (product is 0.72 gram, and yield is 58%).
Embodiment B
Catalyst I I: two (5-phenyl-5,10-dihydro indeno [1,2-b] indyl) dichloro closes the preparation of zirconium
General step by embodiment A makes 1-indone and hydrochloric acid N, and N-phenylbenzene hydrazine reaction is made 5-phenyl-5,10-dihydro indeno [1,2-b] indoles.Form lithium salts with the n-Butyl Lithium reaction then, make this lithium salts make catalyst I I with the zirconium tetrachloride reaction again.
Embodiment C
Catalyst I II: two-(5,8-dimethyl-5,10-dihydro indeno [1,2-b] indyl) dichloro closes the preparation of zirconium
In 250 milliliters of round-bottomed flasks, 180 milliliters of ethanol, 10 milliliters of HCl, 16.3 gram 1-indones (0.124 mole) and 19.5 are restrained hydrochloric acid p-methylphenyl hydrazine (0.124 mole) reflux 6 hours.After being cooled to 25 ℃, filter the precipitation that is produced,,, use twice of 50 milliliters of hexane wash then with 50 ml water washed twice with 100 milliliter of 10% aqueous ethanolic solution washing twice.Obtain 25 gram 8-methyl-5 after the drying, 10-dihydro indeno [1,2-b] indoles.
Add 0.5 gram bromination trimethylammonium cetyltrimethyl ammonium, 6.1 gram 8-methyl-5 to 100 milliliters of 50%NaOH aqueous solution, 10-dihydro indeno [1,2-b] indoles adds 100 milliliters of toluene then under violent stirring.Add methyl-iodide (1.8 milliliters) then.Under 25 ℃, this mixture was stirred 3 hours, then in 100 ℃ of heating 30 minutes.After being cooled to 25 ℃, mixture is divided into two-layer: light yellow organic layer and water layer.Organic layer is separated with water layer, filter in the organic layer and precipitate.Water layer extracts with toluene, then toluene extraction liquid and organic layer is merged, and the mixture after the merging is at Na 2SO 4Last dry, and filter.The filtrate that obtains is concentrated up to forming solid.From solution, isolate solid and merge with the solid product of previous collection.Solid product after the merging is used washing with alcohol earlier, uses hexane wash then, obtains 3.05 grams 5 after the drying, 8-dimethyl-5,10-dihydro indeno [1,2-b] indoles.
Under nitrogen protection, with 1.52 gram (0.0077 moles) 5,8-dimethyl-5,10-dihydro indeno [1,2-b] indoles is dissolved in 15 milliliters of toluene.Add the pentane solution (2.0 mol) of 3.9 milliliters of n-Butyl Lithiums to this solution.Make reflux 3 hours postcooling to 25 ℃ of this mixture then.By filtering to isolate precipitation,, under vacuum, obtain 1.26 grams 5 after the drying, 8-dimethyl-5,10-dihydro indeno [1,2-b] indyl lithium with the hexane wash precipitation.
Under nitrogen protection, with 0.24 gram (0.001 mole) 5,8-dimethyl-5,10-dihydro indeno [1,2-b] indyl lithium is dissolved in 20 milliliters of diethyl ether.This solution is added to lentamente in 20 milliliters of diethyl ether slurry of zirconium tetrachloride (0.12 gram, 0.0005 mole).Stirred this mixture 2 hours down at 25 ℃, filter, wash, under vacuum, obtain 0.23 gram catalyst I II after the drying with diethyl ether.
Embodiment D
Catalyst I V: two (5-trimethyl silyl-8-methyl-5,10-dihydro indeno [1,2-b] indyl) dichloro closes the preparation of zirconium
General step by embodiment A makes 8-methyl-5, and 10-dihydro indeno [1,2-b] indoles and n-Butyl Lithium reaction make the reaction of reaction product and trimethylchlorosilane to form 5-trimethyl silyl-8-methyl-5,10-dihydro indeno [1,2-b] indoles then.Make the reaction of the latter and n-Butyl Lithium to form lithium salts, this lithium salts forms catalyst I V with the zirconium tetrachloride reaction again.
Embodiment 1-12
Polyacrylic preparation with isotactic and atactic block sequence
Polyreaction is to carry out in 1 liter of stainless steel reactor that agitator is housed.At room temperature, propylene (350 milliliters) dry, anaerobic is packed in the reactor of cleaning, dry, anaerobic.Then, specified amount (according to the form below 1) activator is added in the reactor with 50 milliliters of propylene liquids.Reactor is heated to desired temperature of reaction and makes its balance.Then with the catalyzer of aequum in 50 milliliters of propylene liquid injecting reactors with the starting polyreaction.Polyreaction was carried out 1 hour.Last in polyreaction remains propylene in the emptying reactor.From reactor, take out polymkeric substance, place the methyl alcohol soaked overnight, filter then and drying.List polymeric reaction condition and polymer properties in the table 1.
Embodiment 13
Repeat the general step of embodiment 1-12, adopt catalyst I II and MAO activator, but 1/2nd MAO directly add in the reactor, and other 1/2nd MAO mixed with catalyzer before being added to reactor in 30 minutes in advance mutually.The polypropylene of making contains 40% isotactic, five unit groups.
Comparative examples 14
With (5,8-dimethyl-5,10-indeno [1,2-b] indyl) (Cp) ZrCl 2The preparation polypropylene
Repeat the step of embodiment 13, but adopt (Cp) ZrCl of single indenoindole catalyzer (5,8-dimethyl-5,10-indeno [1,2-b] indyl) 2The polypropylene of making only contains 8% isotactic, five unit groups, and the polypropylene that embodiment 13 makes contains 40% isotactic, five unit groups (seeing Table 2).
Table 1
Polymerizing condition and polymer performance
Embodiment Catalyzer Activator Activator/catalyzer Temperature ℃ KgPP/ mol Zr MW a Mw/ Mn a mmmm ％ b T m c ℃
1 2 3 4 5 6 7 8 9 10 11 12 I II III IV I II III IV I I I I MAO MAO MAO MAO MAO MAO MAO MAO MAO MAO MAO * 2000 2000 2000 2000 5000 5000 5000 5000 5000 5000 2000 * 25 25 25 25 25 25 25 25 50 70 50 25 7125 1115 240 430 11750 2060 90 260 4030 5750 3030 5460 75,400 85,900 46,000 59,300 54,100 61,700 19,500 72,200 28,500 9,200 54,500 215,600 2.8 6.1 5.9 3.4 3.3 6.3 6.6 3.4 6.9 6.1 8.8 2.7 50 26 34 28 49 26 - - 50 41 54 20 146.1 150.7 72.7 - 148.4 149.9 - - 147.3 122.2 147.4 128.0
A-is that the GPC of standard measures with the polystyrene
B-uses 13C-NMR measures
C-measures with DSC
*-activator is triisobutyl aluminium and the boratory mixture of trityl four (pentafluorophenyl group), Al/ borate/Zr=300/2/1.
Table 2
Polymerizing condition and polymer performance
Embodiment Catalyzer Activator Activator/catalyzer Temperature ℃ KgPP/ mol Zr MW Mw/ Mn mmmm ％ T m ℃
13 C14 III * MAO MAO 2000 2000 25 25 440 440 34,600 13,800 2.6 2.7 40 8 151.1 -
*-catalyzer is (5,8-dimethyl-5,10-indeno [1,2-b] indyl) (CP) ZrCl 2

Claims (11)

  1. One kind activator and have two non-bridged indenoindole ylidene ligands 3-5 group 4 transition metal catalyzer in the presence of make the method for propylene polymerization, the polypropylene that wherein makes has isotaxy and atactic block sequence, isotactic five unit group mmmm content are in 10 moles of %-70 mole % scopes, and described catalyzer has following structure:
    Figure C028099850002C1
    M is the 3-5 group 4 transition metal in the formula; X 1And X 2Be identical or inequality, be selected from halogen, alkoxyl group, aryloxy, siloxy-, dialkyl amido and hydrocarbyl ligand; L 1And L 2Be identical or inequality, be selected from
    Figure C028099850002C2
    With
    Figure C028099850002C3
    R in the formula 1It is phenyl; R 2To R 10Be identical or inequality, be selected from hydrogen, alkyl, aryl, aralkyl, silyl, halogen, alkoxyl group, aryloxy, siloxy-, thioether, nitro, dialkyl amido and ammonia diaryl base group.
  2. 2. the process of claim 1 wherein that activator is selected from the anionic compound of aikyiaiurnirsoxan beta, aluminum alkyls, alkyl aluminum halide, boron or aluminium, trialkylboron, triarylboron and their mixture.
  3. 3. the process of claim 1 wherein X 1And X 2Be chlorine.
  4. 4. the process of claim 1 wherein that M is a zirconium.
  5. 5. the method for claim 2, wherein activator is an aikyiaiurnirsoxan beta.
  6. 6. the method for claim 2, wherein activator is trialkylaluminium and the boratory mixture of trityl four (pentafluorophenyl group).
  7. 7. the process of claim 1 wherein that described catalyzer has following structure:
    Figure C028099850003C1
    M is the 3-5 group 4 transition metal in the formula; L 1And L 2Be identical or inequality, be selected from
    Figure C028099850003C2
    With
    Figure C028099850003C3
    R in the formula 1It is phenyl; R 2To R 10Be identical or inequality, be selected from hydrogen, alkyl, aryl, aralkyl, silyl, halogen, alkoxyl group, aryloxy, siloxy-, thioether, nitro, dialkyl amido and ammonia diaryl base group; With
    Described activator is an alumoxane activator.
  8. 8. the method for claim 7, wherein M is a zirconium.
  9. 9. the method for claim 7, wherein polyreaction is carried out in temperature is 0 ℃ of-150 ℃ of scope.
  10. 10. the method for claim 7, wherein polyreaction is carried out in temperature is 25 ℃ of-100 ℃ of scopes.
  11. 11. the method for claim 7, wherein said catalyzer has following structure
    Figure C028099850004C1
    The polypropylene that wherein makes has isotaxy and atactic block sequence, and isotactic five unit group mmmm content are in 40 moles of %-60 mole % scopes.
CN02809985.0A 2001-05-17 2002-04-25 Polypropylene preparation Expired - Fee Related CN1273503C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/859,332 US6541583B2 (en) 2001-05-17 2001-05-17 Polypropylene preparation
US09/859,332 2001-05-17

Publications (2)

Publication Number Publication Date
CN1509296A CN1509296A (en) 2004-06-30
CN1273503C true CN1273503C (en) 2006-09-06

Family

ID=25330641

Family Applications (1)

Application Number Title Priority Date Filing Date
CN02809985.0A Expired - Fee Related CN1273503C (en) 2001-05-17 2002-04-25 Polypropylene preparation

Country Status (9)

Country Link
US (1) US6541583B2 (en)
EP (1) EP1389220B1 (en)
CN (1) CN1273503C (en)
AT (1) ATE316985T1 (en)
CA (1) CA2444902C (en)
DE (1) DE60209023T2 (en)
ES (1) ES2257573T3 (en)
MX (1) MXPA03009844A (en)
WO (1) WO2002092647A1 (en)

Families Citing this family (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6908972B2 (en) * 2002-04-16 2005-06-21 Equistar Chemicals, Lp Method for making polyolefins
US6737487B2 (en) * 2002-07-30 2004-05-18 Equistar Chemicals, Lp Polyolefin block copolymers
US8008412B2 (en) 2002-09-20 2011-08-30 Exxonmobil Chemical Patents Inc. Polymer production at supersolution conditions
US6765074B2 (en) * 2002-09-27 2004-07-20 Equistar Chemicals, Lp Olefin polymerization process
US6841500B2 (en) * 2002-12-03 2005-01-11 Equistar Chemicals, Lp Bimetallic indenoindolyl catalysts
US6683150B1 (en) * 2002-12-19 2004-01-27 Equistar Chemicals, Lp High molecular weight polypropylene process
US7183364B2 (en) * 2002-12-20 2007-02-27 University Of Maryland, College Park Process for preparation of polyolefins via degenerative transfer polymerization
US7541412B2 (en) * 2002-12-20 2009-06-02 University Of Maryland, College Park Process for preparation of polyolefins via degenerative transfer polymerization
US20040176241A1 (en) * 2003-03-04 2004-09-09 Sandor Nagy Benzoindenoindolyl metal catalysts for olefin polymerization
US6794468B1 (en) 2003-05-12 2004-09-21 Equistar Chemicals, Lp Olefin polymerization process
US6998451B2 (en) * 2003-07-01 2006-02-14 Equistar Chemicals, Lp Olefin polymerization process
US6933353B2 (en) * 2003-07-07 2005-08-23 Equistar Chemicals, Lp Olefin polymerization process
US6958377B2 (en) * 2003-10-15 2005-10-25 Equistar Chemicals, Lp Olefin polymerization process
US6967231B1 (en) 2004-09-23 2005-11-22 Equistar Chemicals, Lp Olefin polymerization process
WO2006065809A2 (en) * 2004-12-16 2006-06-22 Exxonmobil Chemical Patents Inc. Heteroatom bridged metallocene compounds for olefin polymerization
US7868088B2 (en) * 2005-03-17 2011-01-11 University Of Maryland, College Park Methods for modulated degenerative transfer living polymerization and isotactic-atactic stereoblock and stereogradient poly(olefins) thereby
WO2006102106A1 (en) * 2005-03-17 2006-09-28 University Of Maryland, College Park Methods for modulated degenerative transfer living polymerization and isotactic-atactic stereoblock and stereogradient poly(olefins) thereby
US7667064B2 (en) * 2005-12-14 2010-02-23 Exxonmobil Chemical Patents Inc. Halogen substituted metallocene compounds for olefin polymerization
US7538168B2 (en) 2005-12-14 2009-05-26 Exxonmobil Chemical Patents Inc. Halogen substituted metallocene compounds for olefin polymerization
WO2007070040A1 (en) 2005-12-14 2007-06-21 Exxonmobil Chemical Patents, Inc. Halogen substituted metallocene compounds for olefin polymerization
WO2007070046A1 (en) * 2005-12-14 2007-06-21 Exxonmobil Chemical Patents Inc. Halogen substituted heteroatom-containing metallocene compounds for olefin polymerization
US7868197B2 (en) * 2005-12-14 2011-01-11 Exxonmobil Chemical Patents Inc. Halogen substituted heteroatom-containing metallocene compounds for olefin polymerization
US7550544B2 (en) 2005-12-14 2009-06-23 Exxonmobil Chemical Patents Inc. Halogen substituted metallocene compounds for olefin polymerization
EP1963347B1 (en) 2005-12-14 2011-10-19 ExxonMobil Chemical Patents Inc. Halogen substituted metallocene compounds for olefin polymerization
US8242237B2 (en) 2006-12-20 2012-08-14 Exxonmobil Chemical Patents Inc. Phase separator and monomer recycle for supercritical polymerization process
JP2010529253A (en) 2007-06-04 2010-08-26 エクソンモービル・ケミカル・パテンツ・インク Very homogeneous solution polymerization of propylene
US8318875B2 (en) 2008-01-18 2012-11-27 Exxonmobil Chemical Patents Inc. Super-solution homogeneous propylene polymerization and polypropylenes made therefrom
US7812104B2 (en) * 2008-01-18 2010-10-12 Exxonmobil Chemical Patents Inc. Production of propylene-based polymers
CN103483482B (en) * 2013-10-14 2015-08-05 中国科学院长春应用化学研究所 Functional isotactic polypropylene and preparation method thereof
CN103980395B (en) * 2014-04-30 2016-08-24 中国科学院化学研究所 A kind of super high molecular weight random polypropylene resin that can be used for 3D printing and its preparation method and application
KR101784463B1 (en) 2014-10-06 2017-10-11 주식회사 엘지화학 Rigand compound, metallocene compound, and method for preparation of olefin-based polymer using the same
CN110655623A (en) * 2019-09-19 2020-01-07 天津大学 Preparation of atactic polypropylene-isotactic polypropylene stereoblock polymer by chain shuttling polymerization method

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2241244B (en) 1990-02-22 1994-07-06 James C W Chien Thermoplastic elastomers
IT1256260B (en) 1992-12-30 1995-11-29 Montecatini Tecnologie Srl ATACTIC POLYPROPYLENE
US5594080A (en) * 1994-03-24 1997-01-14 Leland Stanford, Jr. University Thermoplastic elastomeric olefin polymers, method of production and catalysts therefor
WO1996020225A2 (en) 1994-12-20 1996-07-04 Montell Technology Company B.V. Reactor blend polypropylene, process for the preparation thereof and process for preparing metallocene ligands
WO1999024446A1 (en) 1997-11-12 1999-05-20 Montell Technology Company B.V. Metallocenes and catalysts for olefin-polymerisation
US6232260B1 (en) * 1999-10-14 2001-05-15 Equistar Chemicals, L.P. Single-site catalysts for olefin polymerization

Also Published As

Publication number Publication date
ES2257573T3 (en) 2006-08-01
US20020193535A1 (en) 2002-12-19
CA2444902A1 (en) 2002-11-21
CA2444902C (en) 2010-07-06
US6541583B2 (en) 2003-04-01
DE60209023T2 (en) 2006-08-17
CN1509296A (en) 2004-06-30
WO2002092647A1 (en) 2002-11-21
MXPA03009844A (en) 2004-05-24
DE60209023D1 (en) 2006-04-13
EP1389220A1 (en) 2004-02-18
EP1389220B1 (en) 2006-02-01
ATE316985T1 (en) 2006-02-15

Similar Documents

Publication Publication Date Title
CN1273503C (en) Polypropylene preparation
CN1060176C (en) Organometallic fluorenyl compounds, preparation, and use
CN1028532C (en) Catalyst for producing hemiisotactic polypropylene
CN1034125C (en) Metallocene catalysts with lewis acids and aluminum alkyls
CN1061996C (en) Process and catalyst for producing syndiotactic polyolefins
CN1222546C (en) Production of E-P copolymers with single metallocene catalyst and single monomer
CN1070654A (en) High pressure prepares polyacrylic method
CN1112937A (en) Metallocene catalyst systems, preparation and use
CN1140721A (en) Metallocene preparation and use
CN102791746A (en) Method for preparing supported metallocene catalyst and method for preparing polyolefin using the same
CN1291996A (en) Polymeric supported catalysts for olefin polymerization
CN1074421C (en) Metallocene compound
CN1809596A (en) Multi-catalyst system for olefin polymerization
CN1849346A (en) Hydrosilane additives for increased polyolefin molecular weight
CN1671756A (en) Polyolefin block copolymers
CN1069907C (en) Solid catalytic component containing zirconium and cycloalkadienyl groups, process for producing it and process for polymerization of olefins in its presence
CN1769337A (en) Polyolefin composite material and preparation method
CN1111544C (en) Use carrier metallocene catalyst to prepare polyolefinic method
CN101885791B (en) Broad/multimodal distributed polyolefin catalyst, preparation and application thereof
CN1820035A (en) Olefin polymerization process
CN102358761A (en) Olefin polymerization catalyst and preparation method thereof
CN1132856C (en) Catalyst for polymerizing semi-metallocene with olefin and its preparing process and application
CN1073120C (en) Deactivated and reactivated matallocene catalyst systems
CN1466596A (en) Method for producing highly productive supported ionic catalyst for gas phase polymerization
CN1756776A (en) Propylene polymerization process

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20060906

Termination date: 20120425